TiO2 BASED SCRUBBING GRANULES, AND METHODS OF MAKING AND USING SUCH TiO2 BASED SCRUBBING GRANULES

ABSTRACT

TiO 2  based scrubbing granules, and methods of making and using such TiO 2  based scrubbing granules are described. TiO 2 -based scrubbing granules include granulated TiO 2  and about 0.5% to about 20% dry weight inorganic salt binder. Other TiO 2  based scrubbing granules include unsintered granulated TiO 2  and about 0.5% to about 20% dry weight inorganic salt binder. Inorganic salt binder include sodium aluminate. Methods of making TiO 2  based scrubbing granules include i) combining TiO 2  particles with inorganic salt binder to form TiO 2 -binder mixture comprising from about 0.5% to about 20% dry weight binder; ii) granulating the TiO 2 -binder mixture; and drying the granulated TiO 2 -binder mixture to form TiO 2 -based scrubbing granules. Methods of using such TiO 2 -based scrubbing granules include introducing TiO 2 -based scrubbing granules to remove adherent deposits on an inner surface of a reactor or heat exchanger during processes of forming TiO 2  particles and finishing the formed TiO 2  particles into finished pigment products.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application claims priority to provisional application 61/639,624 filed Apr. 27, 2012 titled METHOD OF PRODUCING TIO₂ SCRUBS AND THEIR USE IN TIO₂ MANUFACTURING PROCESSES.

BACKGROUND

1. Field of the Presently Disclosed and/or Claimed Inventive Concept(s)

This invention includes embodiments relating to titanium dioxide (TiO₂) based scrubbing granules, and methods of making and using such TiO₂ scrubbing granules. Particularly, the invention includes embodiments relating to TiO₂ based scrubbing granules with sodium aluminate binder and various methods of using such TiO₂ based scrubbing granules during TiO₂ production; and embodiments relating to unsintered TiO₂ based scrubbing granules with inorganic metal binder and various methods of using such TiO₂ based scrubbing granules during TiO₂ production

2. Background of the Presently Disclosed and/or Claimed Inventive Concept(s)

Generally, TiO₂ particles are produced by a chloride or a sulfate process. In the chloride process, titanium tetrachloride (TiCl₄) undergoes vapor phase oxidation to form TiO₂ particles as part of a hot gaseous suspension. The hot TiO₂ particles, along with other gaseous by-products in the hot gaseous suspension, are passed from a reactor to a heat exchanger. The hot gaseous suspensions are cooled by contact with the inner surface walls of the heat exchanger which have temperatures less than that of the hot gaseous suspension. As the hot TiO₂ particles are cooled, the TiO₂ particles may deposit on the inner walls of the heat exchanger or reactor and form adherent layer deposits. The adherent layer deposits lower heat transfer efficiency through the inner walls of the heat exchanger and thus reduce cooling efficiencies. Such inefficiencies affect the quality of the formed TiO₂ particles and the efficiency of the downstream finishing and surface treatment steps.

In attempts to remove adherent layers, “scrubs” such as sodium chloride (NaCl), silica sand, calcined TiO₂ particles, sintered TiO₂ particles have been added to the hot TiO₂ pigment particles flowing through the reactor and heat exchanger. For example, NaCl scrubs such as U.S. Pat. No. 3,511,308 increase viscosity of TiO₂ slurry, thereby lowering the throughput rate in the finishing step. Silica sand scrubs introduce contaminants into the process and may also increase reactor wear and downtime of the process equipment, e.g., the reactor, the heat exchanger, etc.

U.S. Pat. No. 5,266,108 discloses calcined TiO₂ scrubs typically prepared by heating the TiO₂ particles to a maximum temperature of approximately 1000° C. Unfortunately, such high temperatures decrease the surface area of most known TiO₂ scrubs and makes size of scrubs difficult to control. Calcined or sintered TiO₂ scrubs also have one or more of the following disadvantages. Calcined or sintered TiO₂ scrubs contaminate the finished TiO₂ pigments, thus requiring additional processes. Calcined or sintered TiO₂ scrubs are difficult to reduce to pigmentary size; and calcined or sintered TiO₂ scrubs can affect the dispersion and/or effectiveness of TiO₂ finishing processes.

Thus, a need still exists for improved scrubbing mediums, and method of making and using such improved scrubbing mediums.

BRIEF SUMMARY

Embodiments of the present invention meet these and other needs by providing TiO₂-based scrubbing granules, and methods of making and using such TiO₂-based scrubbing granules.

Accordingly, one aspect of the invention provides TiO₂-based scrubbing granules. The TiO₂-based scrubbing granules include granulated TiO₂ and about 0.5% to about 20% dry weight sodium aluminate binder.

A second aspect of the invention provides TiO₂-based scrubbing granules. The TiO₂-based scrubbing granules include granulated TiO₂ and about 0.5% to about 20% dry weight binder. The binder is selected from a group consisting of sodium aluminate, sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate, and aluminum sulfate, and combinations thereof.

A third aspect of the invention provides TiO₂-based scrubbing granules. The TiO₂-based scrubbing granules include granulated TiO₂ and about 0.5% to about 20% dry weight binder and wherein the TiO₂-based scrubbing granules are unsintered.

A fourth aspect of the invention provides a method of making TiO₂-based scrubbing granules. The method includes: i) combining TiO₂ particles with sodium aluminate binder to form a TiO₂-binder mixture comprising from about 0.5% to about 20% dry weight binder; ii) granulating the TiO₂-binder mixture; and iii) drying the granulated TiO₂-binder mixture to form TiO₂-based scrubbing granules.

A fifth aspect of the invention provides a method of making TiO₂-based scrubbing granules. The method includes: i) combining TiO₂ particles with binder to form a TiO₂-binder mixture comprising from about 0.5% to about 20% dry weight binder; ii) granulating the TiO₂-binder mixture; and iii) drying the granulated TiO₂-binder mixture to form TiO₂-based scrubbing granules. The binder is selected from a group consisting of sodium aluminate, sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate.

A sixth aspect of the invention provides a method of making TiO₂-based scrubbing granules. The method includes: i) combining TiO₂ particles with a binder to form a TiO₂-binder mixture; ii) granulating the TiO₂-binder mixture; and iii) drying the granulated TiO₂-binder mixture to formTiO₂-based scrubbing granules without sintering the TiO₂-based scrubbing granules. The binder comprises from about 0.5% to about 20% by dry weight of the TiO₂-based scrubbing granules.

A seventh aspect of the invention provides a method of using TiO₂-based scrubbing granules. The method includes:

-   -   i. introducing TiCl₄ into a TiO₂ reaction zone of a reactor to         form TiO₂ particles;     -   ii. introducing TiO₂-based scrubbing granules into the reactor         or a heat exchanger, thereby resulting in a TiO₂ product stream         comprising the TiO₂-based scrubbing granules and formed TiO₂         particles; and     -   iii. cooling the TiO₂ product stream via the heat exchanger,         wherein the TiO₂-based scrubbing granules in the TiO₂ product         stream removes deposits on an inner surface of the heat         exchanger as the TiO₂ product stream comprising the TiO₂-based         scrubbing granules passes through the heat exchanger. The         TiO₂-based scrubbing granules include granulated TiO₂ and about         0.5% to about 20% dry weight sodium aluminate binder.

An eighth aspect of the invention provides a method of using TiO₂-based scrubbing granules. The method includes:

-   -   i. introducing TiCl₄ into a TiO₂ reaction zone of a reactor to         form TiO₂ particles;     -   ii. introducing TiO₂-based scrubbing granules into the reactor         or a heat exchanger, thereby resulting in a TiO₂ product stream         comprising the TiO₂-based scrubbing granules and formed TiO₂         particles; and     -   iii. cooling the TiO₂ product stream via a heat exchanger,         wherein the TiO₂-based scrubbing granules in the TiO₂ product         stream removes deposits on an inner surface of the heat         exchanger as the TiO₂ product stream comprising the TiO₂-based         scrubbing granules passes through the heat exchanger. The         TiO₂-based scrubbing granules include granulated TiO₂ particles         and about 0.5% to about 20% dry weight binder. The binder is         selected from a group consisting of sodium aluminate, sodium         sulfate, sodium phosphate, sodium silicate, sodium chloride,         sodium hexametaphosphate, and aluminum sulfate, and combinations         thereof.

A ninth aspect of the invention provides a method making TiO₂ particles. The method includes:

-   -   i. introducing TiCl₄ into a TiO₂ reaction zone of a reactor to         form TiO₂ particles;     -   ii. introducing unsintered TiO₂-based scrubbing granules into         the reactor or a heat exchanger, thereby resulting in a TiO₂         product stream comprising the TiO₂-based scrubbing granules and         formed TiO₂ particles; and     -   iii. cooling the TiO₂ product stream via a heat exchanger,         wherein the TiO₂-based scrubbing granules in the TiO₂ product         stream removes deposits on an inner surface of the heat         exchanger as the TiO₂ product stream comprising the TiO₂-based         scrubbing granules passes through the heat exchanger. The         unsintered TiO₂-based scrubbing granules include granulated and         about 0.5% to about 20% dry weight binder.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a flow chart of a conventional method of making TiO₂-based scrubbing granules;

FIG. 2 is a flow chart of a method of making TiO₂-based scrubbing granules in accordance with an embodiment of the invention;

FIG. 3 is a flow chart of a method of using TiO₂-based scrubbing granules in accordance with an embodiment of the invention; and

FIG. 4 compares crush strengths of comparative examples calcined TiO₂ scrubs A and B and TiO₂ bases scrub granules with NaCl binder in accordance with an embodiment of the invention;

FIG. 5 compares crush strengths of the same comparative examples calcined TiO₂ scrubs A and B with TiO₂ based scrub granules with sodium aluminate as binder without recycle in accordance with an embodiment of the invention;

FIG. 6 compares crush strengths of the same comparative examples calcined TiO₂ scrubs A and B with TiO₂ based scrub granules with sodium aluminate as binder with multiple recycle in accordance with an embodiment of the invention;

FIG. 7 compares crush strengths of TiO₂ based scrub granules with sodium aluminate binder compressed respectively under 13.8 barg, 34.5 barg, and 69 barg roll pressures in accordance with embodiments of the invention;

FIG. 8 compares crush strengths of TiO₂ based scrub granules with sodium aluminate binder compressed under 13.8 barg and dried at respective temperature conditions in accordance with embodiments of the invention;

FIG. 9 compares crush strengths of TiO₂ based scrub granules with sodium aluminate binder compressed under 34.5 barg and dried at respective temperature conditions in accordance with embodiments of the invention;

FIG. 10 compares crush strengths of TiO₂ based scrub granules with sodium aluminate binder compressed under 69 barg dried at respective temperature conditions in accordance with embodiments of the invention;

FIG. 11 is a boxplot comparison of crush strengths of same comparative examples calcined TiO₂ scrubs A and B versus TiO₂ based scrubbing granules with sodium silicate binder, not pressure rolled and dried at 100° C. overnight in accordance with embodiments of the invention; and

FIG. 12 is a boxplot comparison of crush strengths of same comparative examples calcined TiO₂ scrubs A and B versus TiO₂ based scrubbing granules with sodium aluminate binder, not pressure rolled and dried at 100° C. overnight in accordance with an embodiment of the invention

DETAILED DESCRIPTION

In the following description, it is understood that terms such as “top,” “bottom,” “outward,” “inward,” and the like are words of convenience and are not to be construed as limiting terms. Reference will now be made in detail to exemplary embodiments of the invention, which are illustrated in the accompanying figures and examples. Referring to the drawings in general, it will be understood that the illustrations are for describing a particular embodiment of the invention and are not intended to limit the invention thereto.

Whenever a particular embodiment of the invention is said to comprise or consist of at least one element of a group and combinations thereof, it is understood that the embodiment may comprise or consist of any of the elements of the group, individually or in combination with any of the other elements of that group. Furthermore, when any variable occurs more than one time in any constituent or in formula, its definition on each occurrence is independent of its definition at every other occurrence. Also, combinations of substituents and/or variables are permissible only if such combinations result in stable compounds.

DEFINITIONS

The term calcining refers to the heating up of solids to a high temperature, but below the incipient fusion or melting point temperature of the solids. Calcination can result in thermal transition, solids phase transition, and/or removal of volatile fraction(s) from the solids. The volatile fraction(s) that is removed is bound with the solids, and exclude surface volatiles, such as surface water or surface moisture. The chemical composition of the product is typically different from that of the reactant. One example of calcination includes the thermal decomposition of limestone via the following reaction:

CaCO₃(solids)+Heat→CaO(solids)+CO₂(gas)

The term sintering refers to the “welding together” and growth of contact area between solid particles at temperatures near the melting point of the solids. The solids are heated up to their incipient fusion temperature (or eutectic point temperature if the solids contain more than one species of compounds). In this heating process, there is a gradual closing of the voids between the particles and densification typically occurs. The solid particles stick together due to partial melting, and form a solid porous mass. Chemical reaction is not taking place, and the chemical composition of the product(s) is substantially the same as the reactant. Examples of sintering include eutectic phase diagrams published in the literature.

Free flowing solids refers to solids capable of flowing out of containers or bins without the aid of flow enhancers, such as bin vibrators, bin inserts, or special flow-enhancing liners on the bin wall. Free flowing solids also refers to the flow of material from the bin, sticky solids and dry powders that tend to adhere strongly to the surface of bins resulting in poor control of material flow. Whereas, with granular solids that do not stick to the walls, the flow is consistent, controlled and hence, called as free flowing.

TiO₂-Based Scrubbing Granules Embodiment 1

An embodiment of the invention includes TiO₂-based scrubbing granules. The TiO₂-based scrubbing granules include granulated TiO₂ and about 0.5% to about 20% dry weight sodium aluminate binder. In another embodiment, the TiO₂-based scrubbing granules further include one or more inorganic salts. Non-limiting examples of inorganic metal salts include sodium aluminate, sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate, aluminum sulfate, either individually or in combinations of two or more thereof.

In a particular embodiment, the TiO₂-based scrubbing granules are dispersible in finished TiO₂ pigment during a process of making such finished TiO₂ pigment. In yet another embodiment, the TiO₂-based scrubbing granules are free flowing. An advantage of free flowing TiO₂-based scrubbing granules includes ease of introducing TiO₂-based scrubbing granules to a location or place such a reactor or heat exchanger.

In an embodiment, the TiO₂-based scrubbing granules are unsintered. In another embodiment, the TiO₂-based scrubbing granules are uncalcined. An embodiment includes TiO₂ based scrubbing granules having an average size in a range of from about 1 mm to about 25 mm. An embodiment includes TiO₂ based scrubbing granules having a bulk density in a range of from about 800 to about 1800 kg/m³.

It should be appreciated that embodiments of the invention include pre-determined and preselected choice of mean size, size distribution, and hardness to provide adequate scrubbing action tailored for specific processes and methodologies. Embodiments of the invention include varying non-limiting parameters such as drying conditions, type of binders, amount of binder, the type of pressure rolls, and amount of pressure applied, either individually and or in combination of two or more thereof as discussed below.

Embodiment 2

In an embodiment of the invention, TiO₂-based scrubbing granules include granulated TiO₂ and about 0.5% to about 20% dry weight binder. The binder includes one or more inorganic salts such as but not limited to sodium aluminate, sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate, and aluminum sulfate, either individually or in combinations of two or more thereof. In a particular embodiment, the binder comprises sodium aluminate. In a particular embodiment, inorganic metal salt includes substantially sodium aluminate. Similar to as described above, in a particular embodiment, the TiO₂-based scrubbing granules are dispersible in finished TiO₂ pigment during a process of making such finished TiO₂ pigment. In yet another embodiment, the TiO₂-based scrubbing granules are free flowing.

In an embodiment, the TiO₂-based scrubbing granules are unsintered. An embodiment includes TiO₂ based scrubbing granules having an average size in a range of from about 1 mm to about 25 mm. An embodiment includes TiO₂ based scrubbing granules having a bulk density in a range of from about 800 to about 1800 kg/m³.

Embodiment 3

An embodiment of TiO₂-based scrubbing granules include granulated TiO₂ and about 0.5% to about 20% dry weight binder and wherein the TiO₂-based scrubbing granules are unsintered. In an embodiment, the binder comprises sodium aluminate. In another embodiment, the binder includes one or more inorganic salts such as but not limited to sodium aluminate, sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate, and aluminum sulfate, either individually or in combinations of two or more thereof. In a particular embodiment, the binder comprises substantially sodium aluminate. In a particular embodiment, the binder comprises greater than 90% by weight sodium aluminate based on total weight of the binder in the TiO₂-based scrubbing granules.

Similar to as described above, in a particular embodiment, the TiO₂-based scrubbing granules are dispersible in finished TiO₂ pigment during a process of making such finished TiO₂ pigment. In yet another embodiment, the TiO₂-based scrubbing granules are free flowing. An embodiment includes TiO₂ based scrubbing granules having an average size in a range of from about 1 mm to about 25 mm. An embodiment includes TiO₂ based scrubbing granules having a bulk density in a range of from about 800 to about 1800 kg/m³.

Method of Making TiO₂-Based Scrubbing Granules

Embodiment of the invention provide methods of making TiO₂-based scrubbing granules as described above. For illustration and not limitation, an embodiment of making TiO₂-based scrubbing granules is compared to conventional methods as depicted in FIG. 1. A conventional method of making TiO₂-based scrubbing granules includes Step 110 is combining TiO₂ particles with binder to form a TiO₂-binder mixture. The binder does not include sodium aluminate as shown in FIG. 1. Step 120 is compacting, and or granulating and drying the TiO₂-binder mixture. Step 130 is sintering or calcining the TiO₂-binder mixture. In some conventional methods, TiO₂-binder mixture is sintered or calcined, either individually or both.

In contrast to conventional FIG. 1, FIG. 2 describes embodiments of the invention of making TiO₂-based scrubbing granules. FIG. 2 is a flow chart of an embodiment of a method of making TiO₂-based scrubbing granules; and the method is not limited by the order or frequency of the steps unless expressly noted.

The method includes Step 210 combining TiO₂ particles with binder to form a TiO₂-binder mixture comprising from about 0.5% to about 20% dry weight binder.

The method is not limited by the shape, size and kind of TiO₂ particles. Non-limiting examples of TiO₂ particles used to make TiO₂ based scrubbing granules include rutile, anatase, and brookite, either individually or in a combination of two or more thereof. In an embodiment, the TiO₂ particles include rutile phase or anatase phase, either individually or in a combination of two or more thereof. Furthermore, the TiO₂ particles used to make TiO₂ based scrubbing granules may be produced from the chloride or sulfate process, either individually or in combination.

In an embodiment, TiO₂ particles are pigmentary sized particles having an average size greater than 0.20 micron. Furthermore, such TiO₂ pigment particles may be in the form of a finished or intermediate product, either individually or in combinations.

Non-limiting embodiments of binders include as described above. A particular embodiment of making TiO₂-based scrubbing granules includes providing sodium aluminate (NaAlO₂) as binder. Using sodium aluminate binder may have unexpected advantage of TiO₂-based scrubbing granules dispersing in TiO₂ slurry and minimizing contamination in downstream processes.

In an embodiment, TiO₂ pigment particles are premixed with sodium aluminate binder and water such that the binder comprises from about 0.5% to about 5% NaAlO₂ dry weight of the TiO₂— sodium aluminate binder mixture and moisture content is about 4%-8%. Approximate mixing equipment such as a pin mixer or turbulizer may be used to mix TiO₂ and binder to make the TiO2-binder mixture. It should be appreciated that embodiments of the invention include introducing and adjusting the type and amount of binder to achieve a desired strength.

It should be also appreciated that embodiments of the invention include introducing a plurality of binders which differ from each other. Furthermore, the plurality of binders may independently have various characteristics which differ from each other.

Optimally, Step 220 includes compacting the TiO₂-binder mixture under pressure to form the TiO₂-binder mixture into compacted briquettes. For illustration and not limitation, TiO2-binder mixture may be passed through a compacting apparatus such as standard compactors or pressure rolls available in the market

Embodiments of the invention are not limited by how the TiO₂-binder mixture is compacted or by the form, size or shape of the compacted briquettes. The compacted briquettes can be formed by any suitable method. An embodiment includes subjecting TiO₂-binder mixture to sufficient pressure to compact. The TiO₂-binder mixture can be compacted by pressure by any suitable means such as, but not limited to, pressure rolls and presses. A specific embodiment includes counter-rotating pressure rolls. If desired, the pressure rolls can have depressions on the surface of the rolls to facilitate compaction. Non-limiting examples of the form of compacted briquettes include sticks, almonds, bricks, blocks, etc. either individually or in a combination of two or more forms. Furthermore, properties of each compacted briquettes are also independent of other compacted briquettes. For example, the size or shape of the compacted briquettes may have varying dimensions of depth, width, length and may independently vary from embodiment to embodiment.

The compacted briquettes can be used as is, if the particle size of the compacted briquettes is as desired. If the size of the compacted TiO₂ binder briquettes is too large, optimally, Step 230 includes breaking the compacted TiO₂ binder briquettes into TiO₂ binder granules.

Compacted TiO₂ binder briquettes can be broken into smaller size by flake breaker or similar equipment to form TiO₂ binder granules. In an embodiment, the compacted briquettes are broken into TiO₂-binder granules having average size in a range of from about 1 mm to about 25 mm. It should be appreciated that the method includes repeating Step 220 compacting the TiO₂-binder mixture into compacted briquettes and Step 230 breaking the compacted TiO₂ into TiO₂-binder granules as desired.

Step 240 optimally includes screening the TiO₂-binder granules. The TiO₂ binder-granules may be screened based on one or more desired specifications such as size specification and reprocessed. For example, TiO₂-binder granules may be selected by an average size in a range of from about 1 mm to about 25 mm. Step 242 optionally includes recycling the TiO₂ binder granules. Oversized TiO₂ granules such as about >25 mm in size may be passed through milling equipment and undersized granules such as about <1 mm may be recycled to a compaction unit to recompact into compacted briquettes. Upon screening, TiO₂-binder granules of desired size range from about 1 mm to about 25 mm are collected and passed on to be part of the TiO₂ based scrubbing granules.

Step 260 includes drying the TiO₂ binder granules to less than 1% water content to form TiO₂ based scrubbing granules. In a particular embodiment, Step 260 includes drying the TiO₂ binder granules that have been screened for a desired specification such as size to less than 1% water content to form TiO₂ based scrubbing granules. Any suitable drying unit may be used to dry the TiO₂ binder granules and invention is not restricted by how the TiO₂ binder granules are dried. In an embodiment, TiO₂ binder granules are dried to achieve <1% moisture thereby improving the strength of the TiO₂ granules. For example the TiO₂-binder mixture may be dried by to heating at a temperature in a range of from about 90° C. to about 700° C. In an embodiment, drying temperature may be in a range, such as but not limited to from about 90° C. to about 200° C. Additionally, the temperature may be varied and/or selected in a range or value to achieve a desired strength.

Method of making TiO₂-based scrubbing granules optionally, includes Step 250 introducing at least some source of nucleating agent to the TiO₂-binder mixture before step 260 drying the TiO₂-binder mixture into TiO₂ based scrubbing granules. An embodiment includes introducing nucleating agents from 1A metals of the periodic table, either individually or in a combination of two or more thereof. Example of group 1A metals include salts and halides of cesium, either individually or combinations of two or more thereof. The method is not limited by the sequential order or frequency of the steps unless expressly as shown in FIG. 2. An embodiment includes Step 250 introducing nucleating agent simultaneously with step 210 or 220. Another embodiment includes Step 260 introducing nucleating agent sequentially before or after step 220 compacting the TiO₂-binder mixture. An embodiment includes Step 250 introducing nucleating agent before step 220 compacting the TiO₂-binder mixture. It should also be appreciated that embodiments of the invention include introducing a plurality of nucleating agents which differ from each other. Furthermore, the plurality of nucleating agents may independently have various characteristics. A particular embodiment includes introducing a plurality of nucleating agents simultaneously or sequentially before Step 260 drying.

Embodiment 1

As shown in FIG. 2, a particular embodiment of making TiO₂-based scrubbing granules includes: i) combining TiO₂ particles with sodium aluminate binder to form a TiO₂-binder mixture comprising from about 0.5% to about 20% dry weight binder; ii) granulating the TiO₂-binder mixture; and iii) drying the granulated TiO₂-binder mixture to form TiO₂-based scrubbing granules.

Embodiment 2

As shown in FIG. 2, another particular embodiment of making TiO₂-based scrubbing granules includes: i) combining TiO₂ particles with binder to form a TiO₂-binder mixture comprising from about 0.5% to about 20% dry weight binder; ii) granulating the TiO₂-binder mixture; and iii) drying the granulated TiO₂-binder mixture to form TiO₂-based scrubbing granules. The binder is selected from a group consisting of sodium aluminate, sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate.

Embodiment 3

In contrast to conventional method as shown in FIG. 1, embodiments of the invention include making TiO₂-based scrubbing granules without sintering or calcining the TiO₂-based scrubbing granules. A particular embodiment includes: i) combining TiO₂ particles with a binder to form a TiO₂-binder mixture; ii) granulating the TiO₂-binder mixture; and iii) drying the granulated TiO₂-binder mixture to form TiO₂-based scrubbing granules without sintering the TiO₂-based scrubbing granules as shown in FIG. 2. The binder comprises of from about 0.5% to about 20% by dry weight of the TiO₂-based scrubbing granules.

Similar to the embodiments of TiO₂-based scrubbing granules described above, in an embodiment, the bulk density of the unsintered TiO₂ scrubbing granules formed is in the range of from about 800 to about 1800 kg/m³. In a particular embodiment, the unsintered TiO₂-based scrubbing granules are dispersible in TiO₂ slurry during a process of making finished TiO₂ pigment. In another embodiment, the unsintered TiO₂-based scrubbing granules are mixed with finished TiO₂ pigment during a process of making such finished TiO₂ pigment. In yet another embodiment, the unsintered TiO₂-based scrubbing granules are free flowing.

Method of Using TiO₂-Based Scrubbing Granules

Embodiments of the invention also include methods of using the TiO₂ based scrubbing granules described above such as to remove adherent deposits and make finished TiO₂ pigment. FIG. 3 is a flow chart of an embodiment of a method of removing adherent deposits and making finished TiO₂ pigment using one or more of the above described TiO₂-based scrubbing granules. Step 310 includes introducing TiCl₄ into a TiO₂ reaction zone of a reactor to form TiO₂ particles. It is understood to one of ordinary skill in the art that TiCl₄ is oxidized in the reaction zone of the reactor to form TiO₂ particles. Step 320 includes introducing TiO₂-based scrubbing granules into the reactor or a heat exchanger resulting in a TiO₂ product stream comprising the TiO₂-based scrubbing granules and formed TiO₂ particles.

The method is not limited by the order or frequency of the steps unless expressly noted. As shown in FIG. 3, the method is not limited by sequential order or frequency of Step 310 and 320. An embodiment of the method includes introducing TiCl₄ and TiO₂-based scrubbing granules into the reactor simultaneously. Another embodiment includes introducing TiCl₄ and TiO₂-based scrubbing granules into the reactor sequentially.

Embodiments of the invention include Step 320 introducing TiO₂-based scrubbing granules into the reactor before, during or after Step 310 introducing TiCl₄ into a TiO₂ reaction zone. In a particular embodiment, a plurality of TiO₂ based scrubbing granules which differ from each other are introduced into the reactor before, or after introducing TiCl₄ into the TiO₂ reaction zone.

In a sequential embodiment, the method include Step 320 introducing TiO₂-based scrubbing granules into the reactor before Step 310 introducing TiCl₄ into the TiO₂ reaction zone. Another embodiment includes Step 320 introducing TiO₂-based scrubbing granules into the reactor during Step 310 introducing TiCl₄ into TiO₂ reaction zone. Another embodiment includes Step 320 introducing TiO₂-based scrubbing granules into the reactor after Step 310 introducing TiCl₄ into the TiO₂ reaction zone.

An embodiment includes introducing TiO₂-based scrubbing granules having about 0.5% to about 20% dry weight binder; and the binder includes sodium aluminate, sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate, and aluminum sulfate, either individually or in a combination of two or more thereof. In a particular embodiment, the method includes introducing TiO₂-based scrubbing granules having about 0.5% to about 20% dry weight sodium aluminate binder.

It should be appreciated embodiments of the invention include methods of removing adherent deposits by introducing embodiments of the TiO₂-based scrubbing granules described above to one or more locations such as a reactor and or a heat exchanger.

In an embodiment, a plurality of TiO₂ based scrubbing granules which differ from each other are introduced into the reactor or heat exchanger. Furthermore, the plurality of TiO₂ based scrubbing granules may have various characteristics.

Embodiment 1

An embodiment includes introducing unsintered TiO₂-based scrubbing granules into the reactor. In an embodiment, the unsintered TiO₂-based scrubbing granules have from about 0.5% to about 20% dry weight binder; and the binder includes one or more sodium aluminate, sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate, and aluminum sulfate, either individually or in a combination of two or more thereof. In a particular embodiment, the unsintered TiO₂-based scrubbing granules have from about 0.5% to about 20% dry weight sodium aluminate binder.

In an embodiment of the invention, the introduced unsintered TiO₂ scrubbing granules have an average size in a range from about 1 mm to about 25 mm. It should be appreciated that embodiments of the invention include pre-determined and preselected choice of size, distribution, and hardness to provide adequate scrubbing action tailored for specific process and/or methodology. Embodiments of the invention include varying non-limiting parameters such as drying conditions, binder, amount of binder, type of pressure rolls, and amount of pressure applied, either individually and or in combination of two or more thereof as discussed below.

In one embodiment, the bulk density of the unsintered TiO₂ based scrubbing granules introduced into the reactor or heat exchanger is in a range of from about 800 to about 1800 kg/m³. In a particular embodiment, the TiO₂ based scrubbing granules are generally free flowing to simplify introduction of such TiO₂ based scrubbing granules into reactor and/or the heat exchanger.

Embodiment 2

In an embodiment of the invention, the introduced TiO₂-based scrubbing granules include granulated TiO₂ and about 0.5% to about 20% dry weight binder. The binder includes one or more inorganic salts such as but not limited to sodium aluminate, sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate, and aluminum sulfate, either individually or in combinations of two or more thereof. In a particular embodiment, the binder comprises sodium aluminate.

Similar to as described above, in an embodiment, the TiO₂-based scrubbing granules are unsintered. In another embodiment, the TiO2-based scrubbing granules further include one or more inorganic salts. Examples of inorganic metal salt include sodium aluminate, sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate, aluminum sulfate, either individually or in combinations of two or more thereof.

In an embodiment of the invention, the TiO₂-based scrubbing granules have an average size in a range of from about 1 mm to about 25 mm. In one embodiment, the bulk density of the TiO₂-based scrubbing granules is in a range of from about 800 to about 1800 kg/m³. The TiO₂-based scrubbing granules are generally but without limitation, free flowing which facilitates feeding of TiO₂-based scrubbing granules into process equipments such as reactors and heat exchangers.

Step 330 includes cooling the TiO₂ product stream via a heat exchanger. The TiO₂-based scrubbing granules in the TiO₂ product stream removes deposits from an inner wall of the heat exchanger as the TiO₂ product stream comprising the TiO₂-based scrubbing granules passes through the heat exchanger. The TiO₂ based scrubbing granules remove deposits or residues within apparatus such as reactors and heat exchangers used in the production of TiO₂ pigment particles via a chloride process as described here. In addition to removing deposits, TiO₂ based scrubbing granules also increase and/or maintaining heat transfer efficiencies through the inner walls of the heat exchanger.

Embodiments of the invention include adjusting and varying the amount of TiO₂ based scrubbing granules that is introduced (Step 320) to remove adherent layer deposits depending upon particular processing conditions, procedures, functional limitations, etc. within the scope and skills of one of ordinary skill in the art given. An embodiment includes introducing one or more combinations of TiO₂ based scrubbing granules with selected characteristics to provide a predetermined scrubbing efficiency. Furthermore, the introduced TiO₂-based scrubbing granules with the selected characteristics may be altered or changed in response to a change in the predetermined scrubbing efficiency. An embodiment includes increasing or decreasing the amount of introduced TiO₂ based scrubbing granules in response to one or more change in a scrubbing efficiency, either individually or combinations thereof. For example, an embodiment includes decreasing the amount of introduced TiO₂ based scrubbing granules as accumulated adherent deposits on the inner wall of the heat exchanger or reactor decrease or vice versa. Amount of scrubbing granule introduced may also be adjusted based upon the temperature limit of downstream equipment i.e. filter inlet temperatures controls feeding rate of scrubs.

In an embodiments, TiO₂ based scrubbing granules are introduced into the reactor and/or heat exchanger in the range from about 0.5 to about 20 wt. % based on total TiO₂ particle production rate in the reactor. In another embodiments, TiO₂-based scrubbing granules are introduced in a range from about 1 to about 10 wt. % based on total TiO₂ particle production rate in the reactor, to remove accumulated adherent layers and thereby improves heat transfer efficiency. In yet another embodiment, TiO₂ scrubbing granules are introduced in a range from about 1 to about 5 wt. %, based on total TiO2 particle production rate in the reactor. In an embodiment, TiO₂ based scrubbing granules are introduced in an amount such that the reaction mass exiting the heat exchanger will be at a temperature compatible with downstream process equipment such as cyclones, filters, and screw conveyers.

Furthermore, embodiments of the invention optionally include Step 350 introducing a nucleating agent, such as from 1A metals of the periodic table, either individually or in a combination of two or more thereof. Non-limiting examples of nucleating agents include salts and halides of cesium, either individually or in combinations of two or more thereof of. The method is not limited by the order or frequency of the steps unless expressly noted. As shown in FIG. 3, the method is not limited by sequential order or frequency of Step 350.

Optionally, embodiments include Step 350 introducing nucleating agent before, during or after step 320 introducing TiO₂-based scrubbing granules into the reactor. An embodiment of the method includes Step 350 introducing nucleating agent and step 320 introducing TiO₂-based scrubbing granules into the reactor simultaneously. An embodiment of the method includes Step 350 introducing nucleating agent and step 320 introducing TiO₂-based scrubbing granules into the reactor sequentially.

A sequential embodiment includes Step 350 introducing nucleating agent before Step 320 introducing TiO₂-based scrubbing granules into the reactor. Another sequential embodiment includes Step 350 introducing nucleating agent after Step 320 introducing TiO₂-based scrubbing granules into the TiO₂ reaction zone. It should be appreciated that the method includes repeating Step 350 as desired, simultaneously or sequentially.

An embodiment includes introducing nucleating agents from 1A metals of the periodic table, either individually or in a combination of two or more thereof. Example of group 1A metals includes salts and halides of cesium. Salts or halides of cesium may control or reduce the particle size distribution of the TiO₂ finished product. It should be appreciated that one or more group 1A metal nucleating agents can also be used instead of, or as a mixture with KCl as nucleating agents.

Step 340 optionally includes recovering the cooled TiO₂ particles and TiO₂-based scrubbing granules from the TiO₂ product stream after having passed through the heat exchanger. The recovered cooled TiO₂ particles and TiO₂-based scrubbing granules may be recovered such as via a bag filter which separates solid TiO₂ particles from gas. Embodiments of the invention also include various finishing processes to form the recovered TiO₂ particles and TiO₂-based scrubbing granules into finished TiO₂ pigment.

A finishing process includes Step 360 forming some of the recovered TiO₂ particles and TiO₂-based scrubbing granules into finished TiO₂ pigment via dry finishing process.

Another finishing process includes Step 370 introducing some of the recovered TiO₂ particles and TiO₂-based scrubbing granules into a slurry tank to form finished TiO₂ pigment via wet finishing process. Unexpected advantages of using TiO₂ based scrubbing granules include one or more of the following. In an embodiment, the TiO₂-based scrubbing granules are dispersible in the aqueous slurry and disperse into TiO₂ particles such that the TiO₂-based scrubbing granules do not need to be removed. The TiO₂ scrubbing granules are capable of being dispersed within the aqueous slurry without introducing foreign contaminants or oversized TiO₂. The TiO₂-based scrubbing granules may also be interspersed within the finished TiO₂ pigment. Thus, embodiments include finished TiO₂ pigment with interdispersed TiO₂-based scrubbing granules.

Furthermore, the TiO₂-based scrubbing granules may be interspersed within the finished TiO₂ pigment without affecting the quality of the finished TiO₂ pigment. As the TiO₂-based scrubbing granules do not significantly degrade or change the physical and or chemical functionality of finished TiO₂ pigment, the TiO₂-based scrubbing granules have the unexpected advantages of not needing to be separated from the finished TiO₂ pigment, not needing to be recycled, and not needing further processing. An embodiment of the invention includes not separating TiO₂-based scrubbing granules from the finished TiO₂ pigment and the finished TiO₂ pigment may be sold and/or used with the TiO₂-based scrubbing granules as a component thereof.

Furthermore, Applicant has also unexpectedly discovered that NaCl or silica sand scrub may be reduced or replaced with one or more embodiments of TiO₂ based scrubbing granules of the present inventions. NaCl scrubs increase viscosity of TiO₂ slurry, thereby lowering the throughput rate in the finishing step. Silica sand scrubs introduce contaminants into the process and may also increase reactor wear and downtime of the process equipments such as reactors and heat exchangers. An embodiment includes TiO₂ based scrubbing granules substantially free of NaCl. An embodiment includes TiO₂ based scrubbing granules substantially free of silica sand. Unexpected advantages include improved throughput rate in the finishing step and increased operating life of process equipment the reactor, the heat exchanger, etc.

Another unexpected advantage of embodiments of TiO₂ based scrubbing granules of the present invention includes minimizing trace metal pick-up by TiO₂ particles. Embodiments of TiO₂ based scrubbing granules are not as hard as conventional silica sand or sintered TiO₂ as shown in FIG. 1 which tends to abrade the walls of process equipments such as reactors and heat exchangers and result in metal pick affecting the quality of finished TiO₂ product.

EXAMPLES

The following examples illustrate the features of embodiments of the invention and are not intended to limit the invention thereto.

Experimental Results and Analysis

TiO₂ pigment particles and binder were mixed to form a TiO₂-binder mixture; and TiO₂-binder mixture was compacted to form various types of TiO₂-based scrubbing granules in studies.

Lab studies were conducted on two compaction processes, pressure roll compaction using an L-83 compactor from Fitzpatrick Company and compaction using a lab scale DISPERMAT® from VMA-Getzmann. Binders such as sodium aluminate (NaAlO₂), sodium silicate (Na₂SiO₃), and sodium chloride (NaCl) were selected for study. Crush strength tests were used to qualitatively compare TiO2-based scrubbing granules in accordance with embodiments of the invention with comparative calcined TiO₂ scrubs examples A and B. Comparative calcined TiO₂ scrubs examples A and B are calcined sulfate TiO₂ scrub materials with different additives and at calcination temperature of 970° C. to 1020° C. Such calcined TiO₂ scrub materials were manufactured by sulfate TiO₂ manufacturing process. Pressure compaction with the L-83 compactor showed that TiO₂-based scrubbing granules in accordance with embodiments of the invention exhibited similar or higher strength than comparative examples A and B calcined TiO₂ scrubs. Lab studies demonstrate that characteristics and quality of the TiO₂-based scrubbing granules in accordance with embodiments of the invention described above may be affected by, for example, the choice of binder, binder concentration, roll pressure, pre-mixing of binder and pigment prior to pressure rolling, initial moisture content, drying temperature, recycling of fines, either individually or combinations thereof.

Pressure Compaction

Pressure compaction was performed using a Pilot scale pressure roller (L-83 compactor from The Fitzpatrick Company). In a test procedure, an appropriate amount of binder and TiO₂ particles were premixed to form TiO₂-binder mixture in accordance with embodiments of the invention described above. TiO₂-binder mixture was placed on a roller mill for about 45 minutes to achieve uniform mixing of the binder and TiO₂ pigment. The TiO₂-binder mixture was then compacted via a pressure roller at 69 barg roll pressure and at 5 rpm roll speed to form compacted briquettes. The compacted briquettes were then dried in lab oven at 100 C overnight. The compacted briquettes were dried such that it contains <1% moisture. The dried compacted briquettes were then sieved and briquettes greater than 3 mm were selected for crush strength analysis. Compacted briquettes of 3 mm and above were chosen so that a qualitative comparison of crush strength analysis can be done with Cristal A and Cristal B calcined scrubs. Results from the screening experiments are discussed below.

Sodium Chloride as Binder

FIG. 4 shows the crush strength values for compacted briquettes formed with respectively 0.5% and 5% NaCl binder compared to the comparative example A and B calcined TiO₂ scrubs. An increase in strength of the compacted briquettes was observed with increase in binder concentration from 0.5% to 5%. However, the average crush strength in both cases was lower than the crush strength of comparative example A calcined TiO₂ scrub.

Sodium Aluminate as Binder

FIG. 5 shows the crush strength values compacted briquettes formed with respectively 1% and 2% sodium aluminate (“SA”) binder compared to the comparative A and B calcined TiO₂ scrubs. Again, an increase in strength of the compacted briquettes was observed with increase in binder concentration.

Effect of Premixing

Binder and TiO₂ pigment particles were premixed in batches using a mixer DISPERMAT™. During mixing, water was added to attain an initial moisture content of about 7%. With 2.5% sodium aluminate as binder, the average crush strength of compacted briquettes was about three times of the comparative A calcined TiO₂ scrubs as shown in FIG. 6. The term “compacts” as used herein and in the figures refers to briquettes produced by pressure rolling. The briquettes are broken down to granules of required specification. Comparison of FIGS. 5 and 6 shows significant increase in the crush strength of [compacted briquettes formed by pre-mixing of sodium aluminate (“SA”) binder and TiO₂ pigment prior to pressure rolling.

Effect of Roll Pressure and Recycle

The effect of roll pressure and recycling of fines on the quality of briquettes that are formed was studied. 2.5% Sodium aluminate binder (based on previous results with higher crush strength) and TiO₂ pigment particles were premixed and an initial moisture content of about 7% was achieved. Effect of roll pressures of 13.8 barg, 34.5 barg, and 69 barg and recycle of fines or briquettes smaller than 3.3 mm were studied.

FIG. 7 shows pressure rolling and recycling significantly affect the quality of briquettes that are formed. Average crush strength of briquettes formed at roll pressure of 13.8 barg is higher than at roll pressure of 69 barg with or without recycling. However, crush strength for a roll pressure of 34.5 barg is slightly higher than those values obtained at 13.8 barg.

Effect of Drying Temperature

The effect of drying temperature on the quality and strength of compacted briquettes in accordance with embodiments of the invention described above were also studied. The compacted briquettes discharged from the pressure roll was dried at 100° C. (overnight), 300° C. (1 hour), 500° C. (1 hour) and 700° C. (1 hour). TiO₂-binder mixture included 2.5% sodium aluminate binder premixed with TiO₂ pigment with an initial moisture content of about 7%. The TiO₂-binder mixture were compacted into briquettes via pressure roll and respectively dried at 100° C. (overnight), 300° C. (1 hour), 500° C. (1 hour) and 700° C. (1 hour).

FIGS. 8-10 crush data show that, independent of the compacting roll pressure, an increase in drying temperature increases crush strength of the compacted briquettes.

Granulation Studies Using Lab Scale Mixer

In these studies, TiO₂ Spray Dryer Discharge pigment particles, binder, and water were combined. A mixer DISPERMAT™ fitted with a 50 mm high-shear impeller, was used for mixing.

In the test procedure, amounts of binder and TiO₂ pigment were placed in the mixer and mixed at about 300 rpm speed. During mixing, water was added to obtain an initial moisture content of about 6% to 8%. Mixing was continued for about 10-15 minutes or until TiO₂-binder mixture sticking to the mixer was observed. TiO₂-binder granules formed were then dried in an oven at 100° C. overnight. The dried TiO₂ based scrubbing granules was then sieved into different mass fractions. TiO₂ based scrubbing granules larger than 3 mm in size were taken and analyzed for crush strength.

Sodium Silicate as Binder

TiO₂-binder mixture with respectively 1%, 2%, and 3% sodium silicate binder and TiO₂ pigment in accordance with embodiments of the invention were mixed as described above. FIG. 11 shows comparison of crush strength values of TiO₂-based scrubbing granules with respectively 1%, 2%, and 3% sodium silicate binder compared to comparative examples A and B calcined TiO₂ scrubs.

Crush strength values of TiO₂-based scrubbing granules with 1%, and 2% sodium silicate binder are similar to comparative example A calcined TiO₂ scrub, whereas, TiO₂ based scrubbing granules with 3% sodium silicate binder have a lower average crush strength value than the comparative example A calcined TiO₂ scrub, but a higher value than comparative example B calcined TiO₂ scrub.

Sodium Aluminate as Binder

TiO₂-binder mixture with respectively 1%, 2%, and 3% sodium aluminate binder and TiO₂ pigment were mixed as described above. FIG. 12 compares of crush strength values of TiO₂-based scrubbing with respectively 1%, 2%, and 3% sodium aluminate binder. Average crush strength values of TiO₂-based scrubbing granules with 1%, 2% and 3% sodium aluminate binder are higher than comparative examples A and B calcined TiO₂ scrubs.

In general, with all tested binders, the crush strength of the granulated TiO2-based scrubbing granules increased as binder concentration increased from about 0.5% to about 3%. TiO₂-based scrubbing granules formed with sodium aluminate as a binder had higher crush strength values when compared to sodium silicate or sodium chloride as binders. Also, granulated TiO₂-based scrubbing granules with sodium aluminate showed an increased crush strength as (1) binder concentration increased from 0.5% to 2.5%, (2) drying temperature increased from 100° C. to 700° C., (3) granules or briquettes of less than 3.0 mm in size were recycled, and (4) initial moisture content was increased from 3% to 7%.

Pilot Scale Studies

Pilot scale studies were performed at a vendor facility to corroborate the laboratory results described above.

Sodium aluminate was used as the binder for the pilot studies. Two experiments with binder levels of 2.5% and 4% sodium aluminate in accordance with embodiments of the invention described above were conducted. As in Step 210 FIG. 2, sodium aluminate binder was mixed with TiO₂ spray dryer discharge using a mixer Turbulizer™ (model TCJS-8) to form a TiO2-binder mixture. As in Step 220, the TiO₂-binder mixture was compacted using a pilot scale MS-75 compaction system at 454 kg/hour feed rate.

As in Step 230, the compacted briquettes were broken into granules via passing through a flake breaker; Sweco 60″ screener and a Frewitt™ granulator produce TiO₂ binder granules of desired size (e.g., 3.36 mm×1 mm or 2 mm×1 mm). As in Step 240 screening, TiO₂ binder granules smaller than 1 mm were recycled to the feed hopper whereas granules greater than 3.36 mm or 2 mm were recycled to the granulator. The TiO₂-based binder granules meeting the above-noted specifications was collected and dried as in Step 260 to less than 1% moisture by to form TiO₂ based scrubbing granules. TiO₂-based binder granules were dried passing through a 1 m² fluid bed dryer. The strength of the TiO₂-based binder granules produced was tested using an attrition method as described below.

Attrition Test Method:

TiO₂-based binder granules s in accordance with embodiments of the invention were compared to comparative calcined TiO₂ scrubs examples A and B using attrition tests.

The attrition test was run by screening TiO₂ based scrubbing granules using a Ro-Tap® sieve shaker, fitted with screens the same size as or slightly finer than the desired product, for five minutes typically. All fines (smaller than 20 mesh) were discarded. Fifty grams of the product larger than 20 mesh were placed on the 20 m mesh screen with (50) ⅜″ steel balls (171.18 g). The Ro-Tap® sieve shaker was run for five minutes without tapper. The percentage of fines (<20 mesh) found in the pan as a result of the attrition from the steel balls is the attrition number. A lower number indicates harder granules.

The average attrition number of TiO₂ binder granules (undried) and the TiO₂ based scrubbing granule (dried TiO₂ binder granules) at 165° C. were respectively 20% and 1.5%, indicating the desirability of drying to form harder granules. The average attrition value of Comparative example A calcined TiO₂ scrub was 6.7% compared to the 1.5% achieved through an embodiment of the present invention; thus, embodiments of methods of the invention formed harder granules than the comparative example A calcined TiO₂ scrub. The attrition numbers did not change significantly (1.3% vs. 1.5% seen in Table 1 below) when the binder level was increased from 2.5% to 4%, thereby confirming laboratory results described above. Increasing binder levels from 0.5% to 2.5% formed harder TiO₂ based scrubbing granules; but, significant impact was not observed when binder level was increased above 2.5%. In addition, at 4% binder level, processing issues related to caking in the compaction feed hopper was observed. The drying temperature in the fluid bed dryer was varied from about 121° C. to about 165° C.

TABLE 1 Results of pilot study using compactor Test # 1 2 TiO2 Feed Rate (lb/hr) 1,000 1,000 Sodium Aluminate* 2.50% 4.00% MS75 Roll Face Stick Stick MS75 Roll (psi) 500 500 MS75 Roll (rpm) 3.5 3.5 MS75 screw type Straight Straight Screw Speed (rpm) 118 100 Product Attrition Fresh 29.20% 26.80% Product Attrition Cured 1.30% 1.50%

Laboratory finishing process evaluation was conducted using the TiO₂ based scrubbing granule produced through a MS75™ compaction system as described above. As described in FIG. 3, TiO₂-based binder granules were introduced into Oxidizer TiO₂ slurry and processed through sand mills, treatment, drying and milling processes as is typically performed to produce commercially acceptable finished TiO₂ product such as finished TiO₂ pigment. The effect of TiO₂ based scrubbing granules on finished TiO₂ pigment was evaluated for performance in a paint application. Table 2 is a Laboratory Investigation result of Performance Prototype Samples prepared in Lab; Micronized at Pilot Plant using air at 290° C. and TiO₂=0.227 kg/min

Unexpected results show that finished TiO₂ pigment with some of the of TiO₂ based scrubbing granule were substantially identical when compared to finished product TiONA® 595 that did not include the TiO₂ based scrubbing granule. Lab finishing process compatibility studies in Table 2 with TiONA® 595 oxidizer base mixed with 5% TiO₂ based scrubbing granules show that there was no difference in the quality of finished TiO₂ pigment formed when compared to TiONA® 595 without the TiO₂ based scrubbing granules. Such results indicate that the TiO₂-based binder granules do not need to be removed from the finished TiO₂ pigment. Furthermore, results indicate that using sodium aluminate binder does not appear to introduce contamination and/or impart undesirable properties into finished TiO₂ pigment.

TABLE 2 Lab Investigation - Effect of TiO₂-based scrubbing granules on Product Performance Interior Interior high-gloss high-gloss latex paint latex paint Exterior Sample Mean/ IEP Brightness Gloss Tint base Description GSD pH % L Δb 20° 60° % L Δb TiONA 595 ™ 0.280/1.424 7.3 100 0 5 5 100.2 −0.1 Oxidizer base + 5% Scrubs, then sandmilled, surface treated, dried in lab TiONA 595 ™ 0.277/1.409 7.5 100 0.15 4 5 100.2 −0.11 Oxidizer base + 5% Scrubs, then sandmilled, surface treated, dried in lab Baseline -TiONA 595 ™ 0.274/1.401 7.52 100.1 0.05 5 5 100.2 −0.2 oxidizer base as Note: GSD is Geometric Standard Deviation; IEP is Isoelectric Point

Each of the patents, published patent applications, references and articles cited herein is hereby expressly incorporated herein by reference in its entirety.

It will be apparent to those skilled in the art that various modifications and variations can be made in the method and system of the present invention without departing from the spirit or scope of the invention. Thus, it is intended that the presently disclosed and/or claimed inventive concept(s) includes modifications and variations that are within the scope of the appended claims and their equivalents.

While the presently disclosed and/or claimed inventive concept(s) has been described in detail in connection with only a limited number of aspects, it should be understood that the presently disclosed and/or claimed inventive concept(s) is not limited to such disclosed aspects. Rather, the presently disclosed and/or claimed inventive concept(s) can be modified to incorporate any number of variations, alterations, substitutions, or equivalent arrangements not heretofore described but which are commensurate with the scope of the claims. Additionally, while various embodiments of the presently disclosed and/or claimed inventive concept(s) have been described, it is to be understood that aspects of the presently disclosed and/or claimed inventive concept(s) may include only some of the described embodiments. Accordingly, the presently disclosed and/or claimed inventive concept(s) is not to be seen as limited by the foregoing description but is only limited by the scope of the appended claims. 

What is claimed is:
 1. TiO₂-based scrubbing granules comprising: i. granulated TiO₂; ii. sodium aluminate binder comprising from about 0.5% to about 20% by dry weight of the TiO₂-based scrubbing granules.
 2. TiO₂-based scrubbing granules of claim 1, wherein the TiO₂-based scrubbing granules are dispersible in a TiO₂ slurry during a process of making finished TiO₂ pigment.
 3. TiO₂-based scrubbing granules of claim 1, wherein the TiO₂-based scrubbing granules are unsintered.
 4. TiO2-based scrubbing granules of claim 1, further comprising an inorganic salt.
 5. TiO₂-based scrubbing granules of claim 1, further comprising an inorganic metal salt selected from the group consisting of sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate, aluminum sulfate, and combinations thereof.
 6. TiO₂-based scrubbing granules of claim 1, wherein the TiO₂-based scrubbing granules have an average size from about 1 mm to about 25 mm.
 7. A method of making TiO₂-based scrubbing granules comprising: i. combining TiO₂ particles with sodium aluminate binder to form a TiO₂-binder mixture comprising from about 0.5% to about 20% dry weight binder; and ii. granulating the TiO₂-binder mixture; iii. drying the granulated TiO₂-binder mixture to form TiO₂-based scrubbing granules.
 8. The method of claim 7, wherein the binder further comprises an inorganic metal salt.
 9. The method of claim 7, wherein the binder further comprises an inorganic metal salt selected from the group consisting of sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate, aluminum sulfate, and combinations thereof.
 10. The method of claim 7, further comprising compacting the TiO₂-binder mixture under pressure to form the TiO₂-binder mixture into compacted briquettes.
 11. The method of claim 10, further comprising breaking the compacted briquettes into TiO2-binder granules having an average size in a range of from about 1 mm to about 25 mm.
 12. The method of claim 7, wherein drying the TiO₂-binder mixture comprises heating at a temperature in a range of from about 100° C. to about 700° C.
 13. The method of claim 7, wherein the TiO₂ particles are produced by a chloride or sulfate TiO₂ manufacturing process.
 14. The method of claim 7, wherein the TiO₂-based scrubbing granules are unsintered.
 15. A method comprising: i. introducing TiCl₄ into a TiO₂ reaction zone of a reactor to form TiO₂ particles; ii. introducing TiO₂-based scrubbing granules into the reactor or a heat exchanger, thereby resulting in a TiO₂ product stream comprising the TiO₂-based scrubbing granules and formed TiO₂ particles; wherein the TiO₂ based scrubbing granules comprise: a. granulated TiO₂; and b. sodium aluminate binder comprising from about 0.5% to about 20% by dry weight of the TiO₂-based scrubbing granules; and iii. cooling the TiO₂ product stream via the heat exchanger, wherein the TiO₂-based scrubbing granules in the TiO₂ product stream removes deposits on an inner surface of the heat exchanger as the TiO₂ product stream comprising the TiO₂-based scrubbing granules passes through the heat exchanger.
 16. The method of claim 15, wherein the introduced TiO₂-based scrubbing granules are unsintered.
 17. The method of claim 15, further comprising introducing TiO₂-based scrubbing granules comprising an inorganic salt selected from the group consisting of sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate, aluminum sulfate, and combinations thereof.
 18. The method of claim 15, further comprising recovering the cooled TiO₂ particles and TiO₂-based scrubbing granules from the heat exchanger.
 19. The method of claim 18, further comprising finishing the recovered TiO₂ particles into finished TiO₂ pigment via a wet finishing process.
 20. The method of claim 19, comprising finishing the recovered TiO₂ particles by introducing the recovered TiO₂ particles and recovered TiO₂-based scrubbing granules into a slurry tank to form the finished TiO₂ pigment.
 21. The method of claim 19, further comprising not removing the TiO₂-based scrubbing granules from the finished TiO₂ pigment.
 22. The method of claim 15, further comprising introducing a nucleating agent to the TiO₂ reaction mixture before, during, or after the TiO₂-based scrubbing granules are introduced.
 23. The method of claim 22, wherein the nucleating agent comprises a salt or halide of a group IA metal.
 24. The method of claim 22, wherein the nucleating agent is selected from the group consisting of potassium, cesium, and combinations thereof.
 25. The method of claim 22, wherein the nucleating agent is selected from a group consisting of KCl, CsCl, and combinations thereof.
 26. The method of claim 15, wherein the TiO₂-scrubbing granules are free flowing.
 27. The method of claim 15, further comprising altering a selected characteristic of the introduced TiO₂ based scrubbing granules in response to a change in a predetermined scrubbing efficiency.
 28. The method of claim 27, further comprising increasing or decreasing the amount of introduced TiO₂ based scrubbing granules in response to a change in the predetermined scrubbing efficiency.
 29. The method of claim 15, wherein the TiO₂-based scrubbing granules are introduced in an amount in range from about 1% to 10% weight percent of the total TiO₂ production rate in the reactor.
 30. TiO₂-based scrubbing granules of claim 1, wherein the TiO₂-based scrubbing granules have a bulk density in a range of from about 800 to about 1800 kg/m³.
 31. TiO₂-based scrubbing granules comprising: i. granulated TiO₂ ii. binder comprising from about 0.5% to about 20% by dry weight of the TiO₂-based scrubbing granules; and iii. wherein the TiO₂-based scrubbing granules are unsintered.
 32. TiO₂-based scrubbing granules of claim 31, wherein the TiO₂-based scrubbing granules are dispersible in TiO₂ slurry during a process of making finished TiO₂ pigment.
 33. TiO₂-based scrubbing granules of claim 31, wherein the binder comprises an inorganic metal salt selected from the group consisting of sodium aluminate, sodium sulfate, sodium phosphate, sodium silicate, sodium chloride, sodium hexametaphosphate, aluminum sulfate, and combinations thereof.
 34. TiO₂-based scrubbing granules of claim 31, wherein the binder comprises sodium aluminate.
 35. TiO₂-based scrubbing granules of claim 31, wherein the TiO₂-based scrubbing granules have an average size in a range of from about 1 mm to about 25 mm.
 36. TiO₂-based scrubbing granules of claim 31, wherein the TiO₂-based scrubbing granules have a bulk density in a range of from about 800 to about 1800 kg/m³. 